CN103911419B - Method for producing L-valine by combined fermentation of double bacterial strains - Google Patents
Method for producing L-valine by combined fermentation of double bacterial strains Download PDFInfo
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Abstract
The invention discloses a method for producing L-valine by combined fermentation of double bacterial strains, which adopts two bacterial strains, one has high bacterial activity and strong acid producing capability, and the other one produces few by-products of impurity acids. The method comprises the following steps: performing seed amplification culture of the two bacterial strains; performing fermentation culture of the bacterial strain with strong acid producing capability; inoculating the bacterial strain with few by-products of impurity acids into the fermentation liquid when the activity decreases, supplementing nutrient solutions, continuing to perform fermentation; and detecting the valine content and amino acid purity by liquid chromatography. Combined fermentation of double bacterial strains improves the fermentation liquid purity and the acid producing amount.
Description
Technical field
The present invention relates to a kind of biological manufacture Valine technology, relate in particular to a kind of double
The method of Valine is prepared in strain-combined fermentation.
Background technology
Valine, as branched-chain amino acid, is one of essential amino acid, has multiple life
Reason function, is widely used in the system of medicine, food and flavoring agent, animal feed and cosmetics
Make, especially the effect in medical research and treatment, be increasingly subject to pay attention to.Abroad, L-
Valine is the medicine intermediate of synthesis N-acetylvaline, highly purified Valine purposes
Wider, added value is high.Produce Valine both at home and abroad in enormous quantities and all use microbe fermentation method.
At present, Valine production strain is more.Wherein, what some brevibacterium produced in bacterium is important
Metabolic pathway changes less, and therefore metabolic activity is strong, and acid yield is high, but secondary raw heteroacid
Many, especially secondary raw L-Leu, ILE etc., this is to rear extraction high-purity L-figured silk fabrics
Propylhomoserin causes the biggest difficulty.Additionally some production bacterium passes through site directed mutagenesis so that produce bacterium
At the most secondary raw L-Leu of sweat and ILE and the most continuous
Consume the L-Leu in culture medium and ILE so that fermentation liquid purity is high, favorably
In the extraction of high-purity Valine, but acid yield may be unsatisfactory.Therefore, look for
To a kind of purity that can either improve in fermentation liquid, the fermentation process pair of high acid can be reached again
Industrialized production high-purity Valine important in inhibiting.
CN200610013535.8 brevibacterium flavum mutant and for fermentative Production L-figured silk fabrics
The technique of propylhomoserin discloses brevibacterium flavum mutant and for fermentation production of L-valine
Technique.With brevibacterium flavum (Brevibacteriumflavum) HL41 (CICC10135) it is
Set out strain, and selection-breeding has genetic marker (Ile-+Leu-+SGr+ α-ABr+ 2-TAr) prominent
Mutant TV230 so that it is there is the biosynthesis ability of Valine.Dash forward with brevibacterium flavum
Mutant TV230 through spreading cultivation, the extraction step of fermentation culture and Valine can get L-
Valine crude product, the most refined available Valine sterling.But yield is low, purity is low.
Summary of the invention
It is an object of the invention to provide a kind of side by double strain-combined fermenting and producing Valines
Method, utilizes the brevibacterium flavum that acid producing ability is strong and the recombination bacillus coli producing acid purity high to join
Closing fermenting and producing Valine, the method is than the acid yield of single culture and fermentation liquid purity
All it is significantly increased.
The present invention use two strain Valines produce bacterium: brevibacterium flavum and recombination bacillus coli.
Fermentation step is as follows:
(1) brevibacterium flavum is inoculated on seed culture medium, carries out seed amplification culture and obtain
Seed liquor；
(2) recombination bacillus coli is inoculated on seed culture medium, carries out seed amplification culture
Obtain seed liquor；
(3) seed liquor step (1) cultivated accesses in the fermentation medium of bacterium of having gone out ferments
Obtaining fermentation liquid, ferment to thalline vigor and decline, sweat adds sugar liquid；
(4) seed liquor step (2) cultivated accesses in the fermentation liquid in step (3),
And add nutritional solution, continue fermentation.
Specifically, the one that the present invention provides is by double strain-combined fermenting and producing Valines
Method as follows:
(1) strain used is:
Brevibacterium flavum XQ6(Leul,Ilel,AHVr,α-ABhr,2-TAhr)
Recombination bacillus coli, this strain be those skilled in the art commonly use leucine,
Isoleucine nutrition lacks the recombination bacillus coli of type.
(2) preparation seed culture medium
Brevibacterium flavum seed culture medium, glucose 20g, peptone 10g, Semen Maydis pulp
20g, ammonium sulfate 5g, potassium dihydrogen phosphate 0.5g, Magnesium sulfate heptahydrate 0.5g, constant volume 1L,
PH6.8,121 DEG C 20 minutes.
Recombination bacillus coli seed culture medium, glucose 20g, Semen Maydis pulp 35g, sulphuric acid
Ammonium 5g, phosphoric acid (85%) 1.2ml, potassium chloride 1g, Magnesium sulfate heptahydrate 0.5g, L-are bright
Propylhomoserin 70mg, ILE 21mg, constant volume 1L, pH6.8,121 DEG C 20 minutes.
(3) preparation fermentation medium
Glucose 60g/L, aminoacid powder 10g/L, Semen Maydis pulp 20g/L, ammonium sulfate 5g/L,
Potassium dihydrogen phosphate 0.5g/L, Magnesium sulfate heptahydrate 0.5g/L, manganese sulfate 7mg/L, sulphuric acid
Ferrous 7mg/L.
(4) preparation nutritional solution
Yeast extract 9g, phosphoric acid (85%) 2.4ml, potassium chloride 2g, ILE 0.3g,
Constant volume 100ml, 121 DEG C of sterilizings 20 minutes.
(5) two strains are produced bacterium to be respectively connected in respective seed culture medium, cultivate 12-24
Hour, cultivation temperature is brevibacterium flavum 30 ± 2 DEG C respectively, recombination bacillus coli 37 ± 2 DEG C,
During the fermentation, noting controlling oxygen degree of dissolution saturation, when not inoculating with the 0h that ferments, liquid is sent out
The oxygen degree of dissolution saturation of ferment culture medium is set to 100%, and the liquid disappeared under high temperature dwell pressure condition in fact is sent out
The oxygen degree of dissolution saturation of ferment culture medium is set to 0%；By regulation air quantity and fermentation tank speed of agitator
Realize.
(6) fermentation medium is loaded in fermentation tank 121 DEG C of sterilizings 25 minutes, adjusts with ammonia
Joint pH to 6.7, presses 10-15%(m/v by the seed liquor of the brevibacterium flavum in step (5))
Inoculum concentration accesses in fermentation medium, and m/v represents mass volume ratio, following identical.Cultivate temperature
Spending 30 ± 2 DEG C, pH6.7 ± 0.2, early stage oxygen degree of dissolution saturation controls more than 20%, middle and late stage
Control between 5-10%, and stream adds 50-75%(m/v) Glucose Liquid, control residual sugar exist
Between 1.0-1.5%(m/v), continuous fermentation 60-90 hour；
(7) treating that in step (6), brevibacterium flavum was fermented to the later stage, thalline vigor is decreased obviously
After, the recombination bacillus coli seed liquor in step (5) is pressed 25-35%(m/v) inoculation
Amount accesses in the fermentation liquid of step (6), and adds the nutritional solution described in step (4), and
Continue fermentation 16-24 hour.Cultivation temperature 37 ± 2 DEG C, pH6.8 ± 0.2, oxygen dissolves saturated
Degree control between 5-10%, and stream adds 50-75%(m/v) Glucose Liquid, control residual sugar
At 1.0-1.5%(m/v) between.
(8) valine content and aminoacid purity in liquid chromatography detection fermentation liquid is used.
Two kinds of bacterial strains that the present invention uses are respectively provided with the ability of accumulation Valine, Qi Zhonghuang
Color brevibacterium is seepage defect type, and thalline vigor is high, and fermentation and acid ability is strong, but fermentation
Liquid purity is undesirable, is unfavorable for the extraction of high-purity Valine product；And large intestine bar of recombinating
Bacterium is L-Leu and ILE auxotroph, thalline vigor and fermentation and acid ability
Not as good as brevibacterium flavum, but fermentation liquid purity is high, the particularly same ILE of L-Leu
Content is low, beneficially the production of high-purity Valine product.Metabolism due to different strain
Feature is different, and mixed culture can improve fermentation liquid purity, it is possible to put forward high acid amount.This
Invention utilizes double strain-combined fermenting and producing Valine, utilizes double respective advantage of bacterial strain,
Wherein producing high purity product Valine has the leucine of negative effect and isoleucine big
About can be down to original 1/6th and 1/10th so that the productivity of Valine and purity
It is greatly improved, provides the raw material basis of high-quality for manufacturing of Valine crude product.
Detailed description of the invention
The purport of the present invention is to use two strain valines to produce bacterium combined ferment to produce L-figured silk fabrics ammonia
Acid, is described in further detail present disclosure below in conjunction with embodiment, is carried in embodiment
And content not limitation of the invention, in preparation process, each raw-material selection can be because of
Ground suiting measures to different conditions and result be there is no substantial effect.
Embodiment 1:(5L fermentation tank)
1, preparation seed culture medium
Brevibacterium flavum seed culture medium, glucose 20g, peptone 10g, Semen Maydis
Slurry 20g, ammonium sulfate 5g, potassium dihydrogen phosphate 0.5g, Magnesium sulfate heptahydrate 0.5g, constant volume
1L, pH6.8,121 DEG C 20 minutes.
Escherichia coli seed culture medium, glucose 20g, Semen Maydis pulp 35g, ammonium sulfate
5g, phosphoric acid (85%) 1.2ml, potassium chloride 1g, the bright ammonia of Magnesium sulfate heptahydrate 0.5g, L-
Acid 70mg, ILE 21mg, constant volume 1L, pH6.8,121 DEG C 20 minutes.
2, preparation fermentation medium, glucose 60g/L, aminoacid powder 10g/L, Semen Maydis
Slurry 20g/L, ammonium sulfate 5g/L, potassium dihydrogen phosphate 0.5g/L, Magnesium sulfate heptahydrate
0.5g/L, manganese sulfate 7mg/L, ferrous sulfate 7mg/L.
3, the preparation of nutritional solution, yeast extract 9g, phosphoric acid (85%) 2.4ml, potassium chloride
2g, ILE 0.3g, constant volume 100ml, 121 DEG C of sterilizings 20 minutes.
4, fermentation technology
(1) brevibacterium flavum is connected on fresh seed culture medium, cultivates light in 30 DEG C
Density 26 times dilution OD560To 0.3.(OD560After representing that seed liquor dilutes 26 times, at 560nm
Wavelength under measure absorbance, the when that value reaching 0.3 or 0.5, seed liquor cultivate end
Only, can move into fermentation tank, it is an index of reflection cell concentration)；
(2) recombination bacillus coli is connected on fresh seed culture medium, cultivates light in 37 DEG C
Density 26 times dilution OD560To 0.5；
(3) fermentation medium 2700ml is loaded in 5L fermentation tank, 121 DEG C of sterilizings 25 points
Clock, regulates pH to 6.7 with ammonia, and seed liquor 300ml of brevibacterium flavum is accessed fermentation
In culture medium, cultivation temperature 30 DEG C, pH6.7, initial air quantity 2L/h, rotating speed 300rpm,
And control rotating speed according to oxygen degree of dissolution saturation, and make oxygen degree of dissolution saturation between 5-10%, stream adds
70% Glucose Liquid control residual sugar between 1.0-1.5%, continuous fermentation 72 hours；
(4) by colibacillary seed liquor, the Huang of step (3) is added by total inoculum concentration 20%
In color brevibacterium continuous fermentation fermentation liquid after 72 hours, and add nutritional solution continuation fermentation,
Cultivation temperature 37 DEG C, pH6.7, air quantity 2L/h, and control rotating speed according to oxygen degree of dissolution saturation
Making oxygen degree of dissolution saturation between 5-10%, continue fermentation 24 hours, residual sugar controls
Between 1.0-1.5%；
(5) valine content and aminoacid purity in chromatograph of liquid detection fermentation liquid is used,
It puts tank sample Valine content average out to 8.3%, and purity is 95.2%, wherein L-Leu
Purity is 0.23%, and ILE purity is 0.03%.
Embodiment 2:(100L fermentation tank)
1, preparation seed culture medium
Brevibacterium flavum seed culture medium, glucose 60g, peptone 30g, Semen Maydis
Slurry 60g, ammonium sulfate 15g, potassium dihydrogen phosphate 1.5g, Magnesium sulfate heptahydrate 1.5g, constant volume
3L, pH6.8,121 DEG C 20 minutes；
Recombination bacillus coli seed culture medium, glucose 60g, Semen Maydis pulp 105g, sulfur
Acid ammonium 15g, phosphoric acid (85%) 3.6ml, potassium chloride 3g, Magnesium sulfate heptahydrate 1.5g,
L-Leu 210mg, ILE 63mg, constant volume 3L, pH6.8,121 DEG C 20
Minute.
2, preparation fermentation medium, glucose 60g/L, Semen Maydis pulp 20g/L, yeast extract
3g/L, phosphoric acid (85%) 1.2ml/L, potassium chloride 1g/L, ammonium sulfate 5g/L, seven
Water magnesium sulfate 0.5g/L, L-Leu 70mg/L, ILE 21mg/L, sulfur
Acid manganese 7mg/L, ferrous sulfate 7mg/L.
3, the preparation of nutritional solution, yeast extract 180g, phosphoric acid (85%) 48ml, potassium chloride
40g, ILE 3g, constant volume 1L, 121 DEG C of sterilizings 20 minutes.
4, fermentation technology
(1) brevibacterium flavum is connected on fresh seed culture medium, in 30 DEG C of cultivations
26 times of OD of optical density560To 0.3；
(2) escherichia coli are connected on fresh seed culture medium, cultivate light in 37 DEG C
26 times of OD of density560To 0.5；
(3) fermentation medium 54L is loaded in 100L fermentation tank, 125 DEG C of sterilizings 20
Minute, seed liquor 3L of brevibacterium flavum is accessed in fermentation medium,
Cultivation temperature 30 DEG C, pH6.7, initial air quantity 800L/h, rotating speed 200rpm,
And control rotating speed according to oxygen degree of dissolution saturation, make oxygen degree of dissolution saturation exist
Between 5-10%, stream add 70% Glucose Liquid control residual sugar 1.0-1.5% it
Between, continuous fermentation 72 hours；
(4) by colibacillary seed liquor, step (3) is added by total inoculum concentration 20%
Brevibacterium flavum continuous fermentation fermentation liquid after 72 hours in, and add
Nutritional solution continues fermentation, cultivation temperature 37 DEG C, pH6.7, air quantity
1600L/h, and it is saturated to make oxygen dissolve according to oxygen degree of dissolution saturation control rotating speed
Degree, between 5-10%, continues fermentation 24 hours, and residual sugar controls
Between 1.0-1.5%；
(5) use valine content and aminoacid in chromatograph of liquid detection fermentation liquid pure
Spending, it puts tank sample Valine content average out to 7.9%, and purity is 94.8%,
Wherein L-Leu purity is 0.43%, and ILE purity is
0.06%。
Comparative example 1:
(1) brevibacterium flavum is inoculated on fresh seed culture medium, condition of culture
For temperature 30 DEG C, pH6.7, cultivate 26 times of OD of optical density560To 0.3；
(2) seed culture based formulas is with brevibacterium flavum seed culture medium in embodiment 1
Formula, fermentative medium formula is with the fermentation culture basigamy in embodiment 1
Side.
(3) brevibacterium flavum seed liquor is joined fermentation medium with 10% inoculum concentration
In, remaining condition is with embodiment 1.
(4) detection Valine content and Purity are with embodiment 1.Continuous fermentation
It is 7.2% that 72 lab scales put tank product acid (Valine content), and purity is about
91.21%, wherein L-Leu content is 1.89%, and ILE contains
Amount is 0.34%.
Comparative example 2:
(1) being inoculated in by escherichia coli on fresh seed culture medium, condition of culture is
Temperature 37 DEG C, pH6.8, cultivates optical density 26 times dilution OD560To 0.5；
(2) seed culture based formulas is with escherichia coli seed culture basigamy in embodiment 2
Side
Fermentative medium formula is with the fermentative medium formula in embodiment 2.
(3) escherichia coli seed liquor is joined in fermentation medium with 10% inoculum concentration,
Remaining fermentation condition is with embodiment 2；
(4) detection Valine content and Purity are with embodiment 1.Continuous fermentation
Within 50 hours, putting tank product Valine is 2.9%, and purity is about 95.21%,
Wherein L-Leu content purity is 0.24%, and ILE content is pure
Degree is 0.03%.
By embodiment 1,2 and comparative example 1,2 it will be seen that be used alone yellow
Brevibacterium fermenting and producing Valine, its Valine purity is low, particularly L-Leu and
ILE content is high, extracts to high-purity valine and causes difficulty；And individually with restructuring
Escherichia coli fermentation produces Valine, and its yield of L-valine is low.With brevibacterium flavum and
The double strain-combined fermenting and producing Valine of recombination bacillus coli, utilizes double bacterial strain respective
Advantage so that productivity and the purity of Valine are greatly improved, for high-purity Valine
Manufacture the raw material basis that high-quality is provided.Mainly high purity product Valine is produced
There are the leucine of negative effect and isoleucine about can be down to original 1/6th and very
One of.
Claims (4)
1. a method for double strain-combined fermenting and producing Valines, uses two strain valines
Produce bacterium combined ferment to produce, it is characterised in that:
It is brevibacterium flavum and recombination bacillus coli respectively that two strain valines produce bacterium；Fermentation is raw
The step producing valine is as follows:
(1) brevibacterium flavum is inoculated on seed culture medium, carries out seed amplification culture and obtain
Seed liquor；
(2) recombination bacillus coli is inoculated on seed culture medium, carries out seed amplification culture
Obtain seed liquor；
(3) seed liquor step (1) cultivated accesses in the fermentation medium of bacterium of having gone out ferments
Obtaining fermentation liquid, ferment to thalline vigor and decline, sweat adds sugar liquid；
(4) seed liquor step (2) cultivated accesses in the fermentation liquid in step (3),
And add nutritional solution, continue fermentation；
In step (1), condition of culture is, cultivation temperature is 30 ± 5 DEG C, incubation time 16-24
Hour, control the oxygen degree of dissolution saturation of overall process more than 20%；
In step (2), condition of culture is, cultivation temperature is 37 ± 5 DEG C, incubation time 12-18
Hour, control the oxygen degree of dissolution saturation of overall process more than 20%；
Described brevibacterium flavum is seepage defect type: XQ6Leul,Ilel,AHVr,α-ABhr,
2-TAhr, described recombination bacillus coli is L-Leu and ILE auxotroph；
The nutritional solution of described step (4) is prepared by following method:
Yeast extract 9g, phosphoric acid 85%2.4ml, potassium chloride 2g, ILE 0.3g,
Constant volume 100ml, 121 DEG C of sterilizings 20 minutes.
The method of double strain-combined fermenting and producing Valine the most according to claim 1,
It is characterized in that, the seed liquor inoculum concentration being loaded in fermentation tank in step (3) is 8-15%m/v,
Condition of culture is, cultivation temperature is 30 ± 2 DEG C, incubation time 60-90 hour, controls early stage
Oxygen degree of dissolution saturation more than 20%, the oxygen degree of dissolution saturation of middle and late stage controls between 5-10%,
Stream adds glucose, and control fermentation liquid residual sugar is between 1-1.5%m/v, and stream adds sugar concentration and is
50-75%m/v.
The method of the most double strain-combined fermenting and producing Valines,
It is characterized in that, the seed liquor inoculum concentration that step (4) is loaded in fermentation tank is 25-35%m/v,
Condition of culture is, cultivation temperature is 37 ± 2 DEG C, incubation time 16-24 hour, and oxygen dissolves full
With degree control 5-10%, stream add glucose control fermentation liquid residual sugar between 1-1.5%m/v,
It is 50-75%m/v that stream adds the sugar concentration of glucose.
The method of double strain-combined fermenting and producing Valine the most according to claim 1,
It is characterized in that, step (4) uses liquid chromatography detection valine content after fermenting
And aminoacid purity.
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| CN108841884B (en) * | 2018-06-28 | 2021-08-13 | 无锡晶海氨基酸股份有限公司 | Method for producing L-isoleucine |
| CN109486894A (en) * | 2019-01-11 | 2019-03-19 | 内蒙古拜克生物有限公司 | A kind of production method of Valine |
| CN109652490B (en) * | 2019-02-25 | 2019-09-03 | 内蒙古拜克生物有限公司 | A kind of fermentation of L-Leu and isolation and purification method |
| CN113025670B (en) * | 2020-12-25 | 2022-10-21 | 安徽华恒生物科技股份有限公司 | Method for preparing valine |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101235401A (en) * | 2007-02-02 | 2008-08-06 | 上海祥韦思化学品有限公司 | Fermentation method for preparing L-amino acid |
| CN100516230C (en) * | 2003-06-11 | 2009-07-22 | 味之素株式会社 | Method for producing L-amino acid |
| WO2009093703A1 (en) * | 2008-01-23 | 2009-07-30 | Ajinomoto Co., Inc. | Method of producing l-amino acid |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100516230C (en) * | 2003-06-11 | 2009-07-22 | 味之素株式会社 | Method for producing L-amino acid |
| CN101235401A (en) * | 2007-02-02 | 2008-08-06 | 上海祥韦思化学品有限公司 | Fermentation method for preparing L-amino acid |
| WO2009093703A1 (en) * | 2008-01-23 | 2009-07-30 | Ajinomoto Co., Inc. | Method of producing l-amino acid |
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